binders for foundry core sand and other binder applications are produced from the tars resulting from production of bisphenol A.
|
1. A binder comprising the product prepared by dissolving in furfuryl alcohol the bottoms from distillation of 2,2-bis-(4-hydroxyphenyl)propane and reacting therewith paraformaldehyde.
6. A process for preparing a binder composition which comprises dissolving in furfuryl alcohol the bottoms from distillation of 2,2-bis(4-hydroxyphenyl)propane and reacting therewith paraformaldehyde at an elevated temperature.
4. A process for manufacturing foundry sand shapes for use as cores and molds comprising placing a sand mix in a shaping element and hardening the mix in the shaping element, the sand mix comprising sand, an acid catalyst and a binder comprising the product prepared by dissolving in furfuryl alcohol the bottoms from distillation of 2,2-bis-(4-hydroxyphenyl)propane and reacting therewith paraformaldehyde.
7. A process in accordance with
8. A process in accordance with
|
|||||||||||||||||||||||||||||||||||||||||
This invention relates to binder compositions and in particular to binder compositions for core sand and the like used in metal foundries.
The chemical 2,2-bis-(4-hydroxyphenyl)propane, commonly known as bisphenol A, finds numerous uses in the chemical arts. Bisphenol A is produced by the condensation reaction of phenol and acetone and bisphenol A of relatively high purity is obtained from the reaction mixture by distillation. However, it is not economically feasible in commercial practice to distill off all of the bisphenol A. The bottoms from the distillations, called tars, typically contain some pure bisphenol A, phenol, dimers and other more advanced polymers. In the past these tars were of no particular use in the industry and were usually burned as a fuel.
In accordance with the present invention we have found that the tars resulting from distillation of bisphenol A from the condensation reaction of phenol and acetone can be advantageously used to form binders for core sands and the like used in metal foundary operations.
The expression "core sand" is used herein to include sand used in making shapes of all sorts for foundry purposes, including sand shapes which are to be used as mold cores, sand shapes useful in other casting processes, including sand shapes which are made in patterns and cured therein as well as free standing sand shapes which may be cured in conventional ovens or in microwave ovens for any desirable purpose in foundry work.
The core sand binders according to this invention are produced by dissolving a BPA tar in furfuryl alcohol and reacting the mixture with paraformaldehyde. The expression "BPA tar" as used herein means the bottoms resulting after distillation of bisphenol A from the condensation reaction mixture of phenol and acetone. To prepare the binders, a BPA tar is added to furfuryl alcohol in an amount from about 20 50% by weight. Then paraformaldehyde is added to the mixture in an amount from about 15 to about 45% by weight of the BPA tar. Preferably, the amount of paraformaldehyde employed in the binder is about 12 parts of paraformaldehyde to 25 parts of the BPA tar. The BPA tar-furfuryl alcohol-paraformaldehyde mixture is catalyzed with from about 0.5 to 10% by weight of the mixture of sodium hydroxide or sodium carbonate, or potassium hydroxide, potassium acetate, sodium acetate or the like. The mixture is reacted at a temperature on the order of about 100°C to 110°C (approximately reflux temperatures) until the viscosity of the composition reaches a desired level.
The temperature of the reaction is maintained at approximately reflux temperature and to this end liquids such as water or methanol can be added to the mixture. When using methanol to control the reflux temperature, longer reaction times are usually required. Preferably, water in amounts of up to about 4% by weight of the mixture is used to control the reflux temperature. The usable viscosity range is from about 1.7' to 4.0' seconds as measured on the bubble viscometer in accordance with the standard method set forth in the American Society for Testing and Materials, ASTM designation D1545-63. The preferred viscosity range in from about 1.7' to 2.3' seconds. The composition is then neutralized, if necessary, to a pH from about 6 to 7.5 with an effective amount of a suitable acid, such as, for example, formic or toluene sulfonic acid, chloroacetic acid, or any other suitable medium-weak acid. The resulting composition is eminently suitable as a binder for core sands with the binder exhibiting desired short work times and good tensile strengths.
BPA tars are available commercially from various sources, including United States Steep Corporation under the designation Liquibis, Shell Chemical Company under the designation Shell Off-Spec Bisphenol A and the General Electric Company under the designations V-420 and V-435. Typical composition values on these materials are as follows:
| ______________________________________ |
| PERCENT BY WEIGHT |
| BPA p,p' Chro- Phe- IPP o,p' |
| TAR BPA1 |
| man I2 |
| nol3 |
| IPP4 |
| Dimer5 |
| BPA6 |
| BPX-I7 |
| ______________________________________ |
| V-435 |
| 45.6 5.8 1.8 0.2 9.2 15.2 0.2 |
| V-420 |
| 38.1 0.8 0.4 0.2 2.1 0.3 16.8 |
| ______________________________________ |
| ##STR1## |
| ##STR2## |
| ##STR3## |
| ##STR4## |
| ##STR5## |
| or |
| ##STR6## |
| ##STR7## |
| ##STR8## |
The core sand binders of this invention are applied to said in conventional manner and are catalyzed to form a rigid material by acids such as toluene-sulfonic acid, phosphoric acid, benzene-sulfonic acid, xylene-sulfonic acid, as well as other standard acid catalysts known and used in the art. The acid catalysts are used in amounts ranging from about 15 to 30% by weight of the binder. Curing of the binders is accomplished by conventional curing methods.
It is generally preferred to use with the binders of this invention is silane glass or silica adhesion promoter in an amount ranging from about 0.1% to 3% based on the weight of the binder. Such silane adhesion promoters are well known in the art and include, for example, gamma-mercaptopropyltrimethoxysilane, N-beta-(aminoethyl)-gamma-aminopropyltrimethoxysilane, beta-(3,4-epoxycyclohexyl)ethyltrimethoxysilane, gamma-glycidoxypropyltrimethoxysilane, gamma-aminopropyltriphenoxysilane, gamma-aminopropyltribenzoyoxysilane, gamma-aminopropyltrifurfuroxysilane, gamma-aminopropyltri (o-chlorophenoxy)silane, gamma-aminopropyltri (p-chlorophenoxy)silane, gamma-aminopropyltri(tetrahydrofurfuroxy)silane, methyl[2-gamma-triethoxysilypropylamino)ethyl amino]3-propionate in methanol, modified aminoorganosilane, Ureido-silane, mercaptoethyltriethoxysilane, chloropropyltrimethoxysilane, vinyltrichlorosilane, vinyltriethoxysilane, vinyltrimethoxysilane, gamma-methacryloxypropyltrimethoxysilane, gamma-methacryloxypropyltri(2-methoxyethoxy)-silane, gamma-glycidoxypropyltrimethoxysilane, vinyltriacetoxysilane, gamma-mercaptopropyltrimethoxysilane, gamma-aminopropyltriethoxysilane, N-beta(aminoethyl)-gamma-amino-propyltrimethoxysilane.
The present invention will be further described in the following examples.
A binder in accordance with this invention was prepared from a blend of furfuryl alcohol (70 parts) and BPA tar V-435 (30 parts). To 84.4 parts of said blend were added 4 parts of water and 11.6 parts paraformaldehyde. The resulting mix was catalyzed with 0.005 parts sodium hydroxide and heated to reflux temperature (110°C) for 11/2 hours. The reaction continued to a 2.5 second bubble viscosity, ASTM D1545-63. The mixture was then neutralized with formic acid to pH 6. The resulting binder composition had a Brookfield viscosity of 356 centipoises at 25°C and contained 0.4% free formaldehyde and 9.4% water.
The procedure of Example 1 was followed except that BPA tar V-420 was used in lieu of BPA tar V-435. The resulting binder had a Brookfield viscosity of 420 centipoises at 25°C and contained 0.20% free formaldehyde and 9.41% water.
A binder in accordance with the invention was prepared following the procedure of Example 2 using as a catalyst 0.5% by weight of 50/50 solution of sodium hydroxide in water. The reaction was conducted at a temperature of 100°C for 51/2 hours. The resulting binder had a viscosity of 246 centipoises, Brookfield, at 25°C
The BPA tars V-435 and V-420 were commercially available tars obtained from the General Electric Company and analyzed as follows:
| ______________________________________ |
| BPA Tar V-420 |
| BPA Tar V-435 |
| ______________________________________ |
| P,P'-Bisphenol A |
| 60 43.1 |
| O,P'-Bisphenol A |
| 0.25 18.1 |
| Dimers 2.75 10.9 |
| Phenol 0.45 1.4 |
| ______________________________________ |
The work times and tensile strengths of various binders were evaluated. In each test 0.30 parts A-1160 Ureido silane (T.M. Union Carbide Co.) were added to each respective binder. Then 3000 parts Wedron 5025 silica sand were admixed with 30 parts of each respective binder and 20% of a 65% solution of toluene sulfonic acid in water (based on the weight of the binder). The sand-binder-catalyst mixes were charged into a multiple mold shaping element and allowed to cure. The tensile strengths were tested after storage overnight at ambient relative humidity of 63% and in a separate test after storage overnight at 92% relative humidity. The strengths listed are an average of six determinations in each instance.
The work times were determined by observation of a portion of each binder-sand-catalyst mix which was set aside for that purpose. The table below contains the results of these tests.
| TABLE I |
| ______________________________________ |
| Tensile |
| Work strengths (psi) |
| Time 63% 92% |
| Test Binder (minutes) |
| R.H. R.H. |
| ______________________________________ |
| A Binder of Example 1 |
| 12 265 165 |
| B Binder of Example 2 |
| 10 235 160 |
| C Commercial Binder Con- |
| taining 95 parts |
| furfuryl alcohol and |
| 5 parts resorcinol |
| 22 315 250 |
| ______________________________________ |
The above results indicate that the binders of the present invention provided shorter work times which are highly desirable for no-bake foundry systems, while providing comparable tensile strengths to the commercial furfuryl alcohol-resorcinol binder.
This example illustrates the effect of incremental additions of furfuryl alcohol to the binders ofthe present invention.
The binder was prepared using a charge 77.5 parts of 50/50 blend of furfuryl alcohol/BPA tar V-420, 17.4 parts of paraformaldehyde and 5.1 parts water. The mixture was catalyzed with 2 parts of a 50% solution of sodium hydroxide in water. After 30 minutes of reflux at 110°C the bubble viscosity had advanced from 5.7 to 14.4 seconds. The product was then cooled at room temperature and adjusted to a pH of 7.2 with formic acid. Analysis revealed that the binder thus prepared contained 0.32 formaldehyde and 11.4% water with a viscosity of 1500 centipoises.
Five aliquots of this binder (which contains 50/50 blend of furfuryl alcohol to BPA-t) were blended respectively with sufficient furfuryl alcohol to provide the ratios of furfuryl alcohol to BPA tar indicated in Table II. To each respective mix was added 0.3% (based on the weight of the binder) of A-1160 Ureido-silane (Union Carbide Co.). In each test, 30 parts of each furfuryl alcohol-diluted binder was admixed with 3000 parts of Wedron 5025 sand. The sand was pre-catalyzed with 7 parts of 65% toluene sulfonic acid in water.
The tensile strengths and work times were tested by the general method described in Example 4. The immediate tensile strengths were tested after storage overnight at ambient humidity (56%) and in another series of tests after storage overnight at 92% high humidity. The results are listed in Table II.
| TABLE II |
| ______________________________________ |
| Work |
| Furfuryl Alcohol: |
| Time Tensile Strength (psi) |
| BPA Tar (minutes) 56% R.H. 92% R.H. |
| ______________________________________ |
| 50:40(a) |
| 20 376 184 |
| 60:30(a) |
| 25 418 232 |
| 70;20(a) |
| 36 381 242 |
| 80:10(a) |
| 41 339 248 |
| 62;31(b) |
| 8 356 193 |
| ______________________________________ |
| (a) 10% water in final binder mix. |
| (b) 7% water in final binder mix. |
This example illustrates the effect of varying the amount of paraformaldehyde in preparing binders of the invention. The binders were prepared following the procedure of Example 1 with the mix being catalyzed with 1% of a 50/50 solution of sodium hydroxide in water. Reactions were carried out at reflux temperature for 1 to 2 hours.
The tensile strengths of the binders were evaluated according to the procedure of Example 4. In each test 0.30 parts of A-1160 Ureido silane were added to each respective binder. The tensile strengths were tested after storage overnight at a relative humidity of 40% and in a separate test after storage overnight at a 90% relative humidity. The data pertaining to these tests are shown in the following table.
| __________________________________________________________________________ |
| Binder 1 Binder 2 Binder 3 Binder 4 Binder |
| __________________________________________________________________________ |
| 5 |
| % Furfuryl Alcohol |
| 59.6 59.6 59.2 59.6 59.6 |
| % Water 3.9 3.9 3.9 3.9 3.9 |
| % BPA Tar-420 |
| 29.8 27.9 25.4 23.1 19.9 |
| % Paraformaldehyde |
| 6.7 8.6 11.5 13.4 16.6 |
| Ratio BPA Tar-V-420/ |
| Paraformaldehyde |
| 4.45 3.24 2.21 1.72 1.20 |
| Reaction time |
| 120 90 70 120 90 |
| Bubble Viscosity |
| 1.9 1.9 1.7 1.9 1.9 |
| Analysis |
| % Formaldehyde |
| 0.2 0.4 0.2 0.4 2.7 |
| % Water 7.0 8.4 7.8 8.8 8.7 |
| Tensile Strength (psi) |
| 40% RH |
| 90% RH |
| 40% RH |
| 90% RH |
| 40% RH |
| 90% RH |
| 40% RH |
| 90% RH |
| 40% |
| 90% RH |
| 160 135 235 160 290 150 310 190 305 220 |
| __________________________________________________________________________ |
A series of tests were performed to compare the "percent carbon" yield of various cold set furfuryl alcohol-containing resins with the binders of the present invention.
The general method employed to determine "percent carbon" yield was the Conradson Carbon Residue of Petroleum Products method, a standard method provided by the American Society for Testing and Materials, ASTM D189-65.
In each test listed in Table III, a 5 gram sample of the resin listed was weighed into a tared crucible. To each sample was added 10% to a 50% solution of ZnCl2 in water. (The ZnCl2 solution is a heat-activated latent acid catalyst.) The acid catalyzed resins were cured in an oven for 2 hours at 200° F. and then for 16 hours at 300° F. The samples were then removed from the oven and allowed to cool. When cool, the samples were weighed to determine the percent of solids and each sample was then put on a Conradson apparatus and a meeker burner was placed under it. The samples were burned for 30 minutes. The flame was then removed, the samples cooled and reweighed.
The "percent carbon" listed in Table III was determined to be the ratio: Final Weight After Burning/Original Weight.
| TABLE III |
| ______________________________________ |
| Test Resin % Carbon |
| ______________________________________ |
| 1 Furfuryl alcohol + 10% BPA(a) |
| 49.7 |
| 2 Furfuryl alcohol + 10% V-420(b) |
| 44.9 |
| 3 Furfuryl alcohol + 25% V-420(b) |
| 44.8 |
| 4 Furfuryl alcohol BPA-tar-420-para- |
| formaldehyde binder(c) |
| 47.7 |
| ______________________________________ |
| (a) BPA bisphenol A (a cold set mixture of BPA and |
| (b) V-420 (BPAtar Trade designation of the General Electric |
| (c) A resin binder in accordance with the present invention and |
| prepared by the general method set forth in Example 2 with the ratio of |
| furfuryl alcohol:BPA tar:paraformaldehyde being 60:40:11.5 |
This example provides a comparison of a binder of this invention with binders prepared following the procedure of Example 3 using pure samples of bisphenol A and phenol. The testing of the binders was conducted as described in Example 4 and results are shown below.
| __________________________________________________________________________ |
| Work |
| Strip |
| Tensile Strengths |
| Binder Composition |
| % Catalyst % Time |
| Time |
| 90% High |
| 38% AMB |
| __________________________________________________________________________ |
| Furfuryl Alcohol/Pure |
| 1 65% solution of |
| 20 |
| 5 ∼25 |
| 140 215 |
| BPA/Formaldehyde |
| Toluene sulfonic |
| Acid |
| Furfuryl Alcohol/ |
| " 65% solution of |
| " 11 ∼40 |
| 180 255 |
| Phenol/Formaldehyde |
| Toluene sulfonic |
| Acid |
| Binder of Example 3 |
| " 65% solution of |
| " 15 ∼55 |
| 160 230 |
| Toluene sulfonic |
| Acid |
| __________________________________________________________________________ |
A number of binders according to this invention were prepared using Shell Chemical Company Off-Specification Bisphenol A as the BPA tar. This material generally contains approximately 80-88% bisphenol A monomer. The amounts of furfuryl alcohol, Shell Off-Specification Bisphenol A and paraformaldehyde used to prepare the binders and the reaction conditions are shown in the table below. The reactions were catalyzed with 0.5% of 50% solution of sodium hydroxide in water. The tensile strength data shown in the table was obtained following the procedure of Example 4. The first value for tensile strength shown in the table was obtained after storage overnight at a relative humidity of 93 and the second value was obtained after storage overnight at a relative humidity of 40. The viscosity values reported in the table are Brookfield viscosity values at 25°C
| ______________________________________ |
| Charge Binder 1 Binder 2 Binder 3 |
| Binder 4 |
| ______________________________________ |
| % Furfuryl |
| Alcohol 57.73 67.67 58.05 53.52 |
| % Shell Off- |
| Spec BPA 26.90 18.86 18.86 33.01 |
| % Paraformalde- |
| hyde 11.54 9.61 19.23 9.60 |
| Ratio Off-Spec |
| BPA/Para- |
| formaldehyde 2.33/1 1.96/1 0.98/1 3.44/1 |
| Product |
| Reaction time |
| at Reflux 80 mins 165 mins 95 mins |
| 60 mins |
| % Formaldehyde |
| 0.44 0.22 4.67 0.47 |
| % Water 10.01 8.77 10.59 9.96 |
| Viscosity (cps) |
| 222.5 111.5 190.5 204.0 |
| Tensiles (psi) |
| 325/420 380/500 345/425 |
| 300/425 |
| 290/360 335/460 290/375 |
| 200/285 |
| ______________________________________ |
A number of binders according to this invention were prepared using United States Steel Corporation Liquibis as the BPA tar. This material generally contains approximately 35% free phenol. The amounts of furfuryl alcohol, Liquibis and paraformaldehyde used to prepare the binders and the reaction conditions are shown in the table below. The reactions were catalyzed with a 50% solution of sodium hydroxide in water as shown in the table. The tensile strength data shown in the table was obtained following the procedure of Example 4. The first value of tensile strength shown in the table was obtained after storage overnight at a relative humidity of 22 and the second value was obtained after storage overnight at a relative humidity of 86.
| ______________________________________ |
| Charge Binder 1 Binder 2 Binder 3 |
| ______________________________________ |
| % Furfuryl Alcohol |
| 62.85 62.85 66.78 |
| % Liquibis 20.95 20.95 22.27 |
| % Paraformaldehyde |
| 12.20 12.20 6.9 |
| Ratio Liquibis/ |
| Paraformaldehyde |
| 1.72 1.72 3.23 |
| % 50% Sodium Hydroxide |
| 2.0 2.0 0.5 |
| Product |
| Viscosity 3.5 sec 1.7 sec 0.8 sec |
| Reaction Time 2.5 hrs 1.5 hrs |
| % Formaldehyde 0.25 0.81 0.31 |
| % Water 10.8 9.12 7.67 |
| Tensile Strength |
| (psi) 22 RH 227 262 203 |
| 86 RH 112 147 131 |
| ______________________________________ |
Compositions in accordance with the present invention have wide applicability as binders not only in the metal founding art but also in other similar applications in which resinous binders are employed, such as for the production of carbon articles such as carbon seals, carbon vanes and reclaimed coke, and for the production of composite articles such as fiberglass and the like. The following examples are representative of additional binder applications.
Approximately 2% of triethylenetetramine (TETA) and 70-75% carbon particles are thoroughly blended. To this dry amine-carbon mixture is added 16-23% of a liquid mixture of a "BPA bar" binder prepared as described above and adjusted to a viscosity of 2500 centipoises by the addition of furfuryl alcohol. The mixing apparatus is cooled throughout the blending of the ingredients. Within about 10 minutes of the addition of the resin binder system, the temperature of the resulting mixture starts dropping gradually from a peak of 50°-60°C Mixing of the ingredients is continued for a total of twenty minutes when a dry, free-flowing particulate solid is obtained.
The free-flowing powder was later placed into a preheated (60°-65°C) extruder and extruded through a die into rods. The green carbon rods were baked and thoroughly carbonized by baking in a reducing atmosphere with a programmed temperature rise to 650°C and holding at that temperature for 48 hours. When carbonized, the rods and satisfactory density and resistivity for use as electrode. No bleeding or cracking was observed. The stack gases from the carbonization furnace were reduced in objectionable gases.
Twelve hundred grams of calcined anthracite were mixed with 150 grams of a "BPA tar" binder prepared as set forth above, 150 grams of furfuryl alcohol and 30 grams of zinc chloride (50% ethanol solution). The above mixture is mixed to a uniform consistency and diluted with furfuryl alcohol, if necessary, to a viscosity of 200 centipoises, Brookfield at 25°C The resulting mixture was compacted or tamped into place between two carbon blocks, cured at 200° and carbonized in a programmed temperature rise to 1000°C at 10°C per hour. The resulting carbonized assembly was tested for tensile force, i.e., the force required to pull the ramming mix from the carbon block. A high adhesion or bond of the block to the ramming mix was noted.
Those modifications and equivalents which fall within the spirit of the invention are to be considered a part thereof.
Doyle, James E., Lembke, Russell B.
| Patent | Priority | Assignee | Title |
| 5612392, | May 16 1995 | ASK CHEMICALS L P | Heat cured foundry binder systems and their uses |
| 6716729, | Dec 22 1999 | WILMINGTON SAVINGS FUND SOCIETY, FSB, AS THE CURRENT COLLATERAL AGENT | Stable bisphenolic compositions |
| Patent | Priority | Assignee | Title |
| 3058954, | |||
| 3403721, | |||
| 3409579, | |||
| 4108809, | Nov 29 1976 | BASF Corporation | Novel prepolymers, flame retardant interpolymers prepared therefrom, and processes for the preparation thereof |
| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
| Dec 09 1980 | DOYLE JAMES E | QUAKER OATS COMPANY, THE, A CORP OF NJ | ASSIGNMENT OF ASSIGNORS INTEREST | 003861 | /0006 | |
| Dec 09 1980 | LEMBKE RUSSELL B | QUAKER OATS COMPANY, THE, A CORP OF NJ | ASSIGNMENT OF ASSIGNORS INTEREST | 003861 | /0006 | |
| Dec 17 1980 | The Quaker Oats Company | (assignment on the face of the patent) | / | |||
| Mar 26 1984 | QUAKER OATS COMPANY A CORP OF NJ | QO CHEMICALS INC CHICAGO ILLINOIS | ASSIGNMENT OF ASSIGNORS INTEREST | 004253 | /0684 | |
| Apr 09 1984 | QO CHEMICALS, INC , | CITIBANK, N A | LICENSE SEE DOCUMENT FOR DETAILS | 004255 | /0547 | |
| Feb 09 1987 | CITIBANK, N A | QO CHEMICALS, INC | RELEASED BY SECURED PARTY SEE DOCUMENT FOR DETAILS | 004754 | /0123 |
| Date | Maintenance Fee Events |
| Oct 08 1985 | REM: Maintenance Fee Reminder Mailed. |
| Oct 09 1985 | REM: Maintenance Fee Reminder Mailed. |
| Mar 09 1986 | EXP: Patent Expired for Failure to Pay Maintenance Fees. |
| Date | Maintenance Schedule |
| Mar 09 1985 | 4 years fee payment window open |
| Sep 09 1985 | 6 months grace period start (w surcharge) |
| Mar 09 1986 | patent expiry (for year 4) |
| Mar 09 1988 | 2 years to revive unintentionally abandoned end. (for year 4) |
| Mar 09 1989 | 8 years fee payment window open |
| Sep 09 1989 | 6 months grace period start (w surcharge) |
| Mar 09 1990 | patent expiry (for year 8) |
| Mar 09 1992 | 2 years to revive unintentionally abandoned end. (for year 8) |
| Mar 09 1993 | 12 years fee payment window open |
| Sep 09 1993 | 6 months grace period start (w surcharge) |
| Mar 09 1994 | patent expiry (for year 12) |
| Mar 09 1996 | 2 years to revive unintentionally abandoned end. (for year 12) |